US4051212A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the continuous degradation of plastics
Assignee: Bayer AG
•
Filing: 1975-08-29
•
Granted: 1977-09-27
•
Expires: 1995-08-29
Abstract
Abstract The instant invention relates to a continuous process for the hydrolytic degradation of plastics wherein a hydrolyzable material is introduced with water into a screw machine, and is subjected therein to a temperature of 100 to 300° C, and a pressure of 5 to 100 bars for 2 to 100 minutes. The invention also relates to an apparatus useful in conducting the process.
Inventors
- 👤 Ernst Grigat
- 👤 Hartmut Hetzel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 18:33
CPC Classifications
C; C08; C08J; C08J11/00; C08J11/04; C08J11/10; C08J11/14; B; B29; B29C; B29C48/00; B29C48/25; B29C48/36; B29C48/50; B29C48/76; B29C48/765; B29C48/766; B29C48/03; Y; Y02; Y02W; Y02W30/00; Y02W30/50; Y02W30/62; Y10; Y10S; Y10S264/00; Y10S264/911; Y10S264/916
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
163 words
A process for the continuous hydrolytic degradation of waste plastics comprising a. continuously introducing a hydrolyzable plastic waste material into a screw machine, b. continuously allowing air to escape from said screw machine, c. continuously introducing water into said screw machine, thereby producing a plastic-water mixture, d. subjecting said mixture to a temperature of from 100° to 300° C, a pressure from 5 to 100 bars, and intensive screw mixing in a reaction zone of said screw machine for a period of from 2 to 100 minutes whereby liquid and gaseous hydrolysis products are formed, e. continuously allowing the liquid and gaseous hydrolysis products to enter a liquid-gas separatory nozzle, f. continuously allowing the liquid to leave the nozzle through a first regulating valve which maintains a constant liquid level in the nozzle, and g. continuously allowing the gas to leave the nozzle through a second regulatory valve which maintains a constant pressure in the nozzle at a pressure of the reaction zone.
Claim 2
Dependent Claim
163 words
A process for the continuous hydrolytic degradation of waste plastics comprising a. continuously introducing a hydrolyzable plastic waste material into a screw machine, b. continuously allowing air to escape from said screw machine, c. continuously introducing water into said screw machine, thereby producing a plastic-water mixture, d. subjecting said mixture to a temperature of from 100° to 300° C, a pressure from 5 to 100 bars, and intensive screw mixing in a reaction zone of said screw machine for a period of from 2 to 100 minutes whereby liquid and gaseous hydrolysis products are formed, e. continuously allowing the liquid and gaseous hydrolysis products to enter a liquid-gas separatory nozzle, f. continuously allowing the liquid to leave the nozzle through a first regulating valve which maintains a constant liquid level in the nozzle, and g. continuously allowing the gas to leave the nozzle through a second regulatory valve which maintains a constant pressure in the nozzle at a pressure of the reaction zone.
Claim 3
Dependent Claim
18 words
The process of claim 1, wherein the machine used comprises inter-engaging screw shafts rotating in the same direction.
Claim 4
Dependent Claim
18 words
The process of claim 2, wherein the screw shafts are fitted with kneading discs in the reaction zone.
Claim 5
Dependent Claim
17 words
The process of claim 1 wherein the water is introduced into the screw machine through a nozzle.
Claim 6
Dependent Claim
41 words
The process of claim 1, wherein the air introduced with the plastic waste is removed through a bore in the housing which is arranged in front of the feed hopper for the plastics material and to which a vacuum is applied.
References Cited (Backward Citations)
US2838801A
Cited
US3229445A
Cited
US3225094A
Cited
US3551943A
Cited
US3499952A
Cited
US3703488A
Cited
US3917507A
Cited
DE2362920A1
Cited
DE2362921A1
Cited
DE2362919A1
Cited
US3959357A
Cited
US3954681A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-09-26 | 1981-03-28 | 1981-09-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-09-26 | 1985-03-28 | 1985-09-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-09-26 | 1989-03-28 | 1989-09-27 | $7700.00 | Window Closed / Lapsed |